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EP 1 103 579 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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23.10.2002 Bulletin 2002/43 |
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Date of filing: 23.11.1999 |
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A process for the extraction of lycopene
Verfahren zur Extraktion von Lycopin
Procédé d'extraction de lycopène
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Designated Contracting States: |
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AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
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Date of publication of application: |
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30.05.2001 Bulletin 2001/22 |
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Proprietor: SOCIETE DES PRODUITS NESTLE S.A. |
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1800 Vevey (CH) |
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Inventors: |
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- Bortlik, Karlheinz
1073 Savigny (CH)
- Mortezavi, Laure
1009 Prilly (CH)
- Saucy, Françoise
1807 Blonay (CH)
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Representative: Thomas, Alain et al |
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55, avenue Nestlé 1800 Vevey 1800 Vevey (CH) |
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References cited: :
EP-A- 0 252 501 WO-A-96/13178 WO-A-98/43620
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EP-A- 0 818 225 WO-A-97/48287
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
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[0001] The present invention concerns a process for the extraction of lycopene.
[0002] Lycopene,which belongs to the family of the carotenoids, is an important natural
food coloring agent in the red region. Lycopene is present naturally in a number of
fruits, primarily in tomatoes and watermelon. It is possible to extract this coloring
agent by different extraction processes. The US Patent No. 4'781'936 for example,
concerns already a process for isolating a yellow coloring component from tomato peel,
which comprises exposing tomato peel to a non-toxic polar extraction solvent, said
solvent being ethanol, lower alcohols, ethers, ketones and aldehydes. The pure lycopene
compound has more a red color, whereas the product obtained by this above mentioned
process allows the production of a final compound having more a yellow color. The
reason of this difference is that according to this process, it is not possible to
obtain a real pure lycopene compound , but more a mixture of the different carotenoids
present in the basic raw material. The European Patent Application EP 0 818 225 A
relates to a process for the preparation of pure lycopene or of lipophilic extracts
containing it from tomatoes. This process involves extraction with aliphatic or aromatic
hydrocarbons or water-immiscible solvents in the presence of phospholipids as surfactant
and stabilizing agents.
[0003] The aim of the present invention is to develop a process, wherein it is possible
to have mainly the extraction of lycopene with a high yield of extraction of said
lycopene.
[0004] The invention concerns a process for the extraction of lycopene from a product taken
in the group consisting of tomato, tomato pomace, pink grapefruit, watermelon, guava
and papaya, wherein said process comprises the following steps :
- removing the impurities and water from the product by subjecting the product to at
least one washing with boiling ethanol, said ethanol having a water content from 20
to 30 %,
- extracting the purified product by subjecting said product to at least one extraction
with boiling ethanol having an alcohol content of at least 92 %,
- recovering the ethanol solution and cooling said solution to a temperature around
the room temperature to obtain lycopene crystals and
- filtrating said solution to recover the lycopene crystals.
[0005] The basic product to be extracted according to the invention is more preferably tomato
or tomato pomace. Under tomato pomace in the present specification, it is to be understood
an industrial waste material from tomato paste production. This tomato pomace includes
the peels and the seeds. Tomato can be every type of tomatoes available in the world.
[0006] It is important according to the process of the invention to have a preliminary washing
of the product to be extracted. The reason is to remove the more polar compounds,
as xanthophylls, the polar carotenoids, and also in the case of the extraction of
tomato pomace, the pesticides present in the peel slurry. This washing is carried
out with ethanol, at the boiling temperature of said ethanol. A further important
condition is to have a water content of the ethanol comprised between 20 and 30 %,
more preferably around 28 %, to avoid any possibility to dissolve the lycopene. The
duration of said washing is normally comprised between 15 and 40 minutes, more preferably
around 30 minutes. All the percentages in the present specification are given in weight.
The washing is made with an excess of boiling ethanol : the ratio ethanol/product
to be extracted is normally around 15:1.
[0007] It is possible to proceed with a single washing of the product. The washing can be
also carried out in two steps, wherein said washings are done in order to have a water
content between 20 and 30 %. For the washings, the water content is preferably around
28 %. The duration of the second washing is the same as the first one, also at the
same temperature.
[0008] At this stage, it is possible to begin the real extraction on the base of the purified
product. The ethanol phase from the washing can be distillated to be used again, for
example for the extraction step. The conditions to have an efficient extraction of
the product is to work with an ethanol having an alcohol content of at least 92 %,
most preferably from 92 to 96 % and at the boiling temperature of said ethanol. Whereas
a sufficiently high temperature is easy to reach, the ethanol produced by distillation
of the filtrates obtained during the 2 purification steps has a too low concentration.
An installation for rectification is necessary for producing adequate ethanol. Accordingly,
commercial ethanol is preferably used in the lycopene extraction process. The extraction
temperature is normally comprised between 70 and 75 °C and the duration is between
2 and 10 minutes at an alcohol content of 94 %.
[0009] A one-step extraction can be sufficient. In order to increase the yield of extraction,
a second extraction with the ethanol of the first step can be carried out. The different
conditions of duration, temperature and content of water of the ethanol used are the
same as for the first extraction step. At the end of the extraction, the spent product
is discarded and the ethanol solution is left either to cool from itself, or cooled
with any cooling medium to reach a temperature between 4 °C and room temperature.
The solution is left overnight , that is during 2 to 12 hours, so that crystals of
lycopene appear.
[0010] These crystals are then isolated from the cold ethanol by filtration or any other
way. The crystals has a deep red colour, which makes clear that the main compound
is lycopene.
[0011] The process of extraction according to the invention allows to reach a yield of more
than half of the initial amount of lycopene. By considering the specific example of
tomato pomace, the concentration of lycopene varies from 28 µg to 1700 µg of lycopene/g
of dry material.
[0012] The obtained lycopene crystals are then ready to be used. This compound is a multifunctional
natural food ingredient. It is first a colorant for drinks, pasta, ice cream and cereals.
It is secondly an efficient antioxydant. Finally, lycopene is biologically active
by contributing to the antioxydative defense system of the organism. It is also responsible
for the reduction of cancer risk and cardiovascular disease. Lycopene can be used
alone or in admixtures with beta-carotene, alpha-tocopherol or flavonoids.
[0013] The following of the specification is now made in relation with the example.
Example
[0014] 300 kg of tomato peel slurry were introduced in an extractor and mixed with 413 kg
of 94 % ethanol. The presence of water in the tomato peel slurry gives an ethanol
having around 72 % ethanol. The mixture was boiled for 15 min. under stirring with
reflux at 74 °C and filtered at 70 °C. The precipitate was mixed with 130 kg of demineralised
water and 316 kg of 94 % ethanol, and boiled for 15 min under stirring with reflux
at 74 °C. The mixture was filtered at 70 °C.
[0015] The purified peel slurry was extracted for 30 min. successively with 220 kg, 220
kg and finally 250 kg of 94 % ethanol under stirring with reflux at 72 °C and filtrated.
The 3 filtrates were pumped into the evaporator, mixed well at 70 °C and finally transfered
to a separated tank. The tank was left overnight at about 10 °C for lycopene crystallization.
Lycopene was filtered at 10 °C with a Seitz filter. About 22.2 g of lycopene were
recovered.
1. A process for the extraction of lycopene from a product taken in the group consisting
of tomato, tomato pomace, pink grapefruit, watermelon, guava and papaya, wherein said
process comprises the following steps :
- removing the impurities and water from the product by subjecting the product to
at least one washing with boiling ethanol, said ethanol having a water content from
20 to 30 %,
- extracting the purified product by subjecting said product to at least one extraction
with boiling ethanol having an alcohol content of at least 92 %,
- recovering the ethanol solution and cooling said solution to a temperature around
the room temperature to obtain lycopene crystals and
- filtrating said solution to recover the lycopene crystals.
2. A process according to claim 1, wherein the removing of the impurities is carried
out during 5 to 40 minutes.
3. A process according to any of claims 1 or 2, wherein for the removing of the impurities
the ratio ethanol/product is around 15:1.
4. A process according to any of claims 1 to 3, wherein the removing of the impurities
is carried out with two ethanol treatments.
5. A process according to any of claims 1 to 4, wherein the extraction of the purified
product is carried out during 2 to 10 minutes with an ethanol having an alcohol content
of 94 %.
6. A process according to claim 5, wherein two extractions are carried out with ethanol.
7. A process according to any of claims 1 to 6, wherein the recovering of the lycopene
crystals is carried out at a temperature comprised between 4 °C and room temperature
during 2 to 12 hours.
1. Verfahren zur Extraktion von Lycopin aus einem Produkt der Gruppe, die besteht aus
Tomate, Tomatentrester, roter Grapefruit, Wassermelone, Guave und Papaya, wobei das
Verfahren die folgenden Schritte umfaßt:
- Entfernen der Verunreinigungen sowie von Wasser aus dem Produkt, indem man das Produkt
wenigstens einem Waschen mit siedendem Ethanol unterzieht, wobei das Ethanol einen
Wassergehalt von 20 bis 30% aufweist,
- Extrahieren des gereinigten Produkts dadurch, daß man das Produkt wenigstens einer
Extraktion mit siedendem Ethanol mit einem Alkoholgehalt von wenigstens 92% unterzieht,
- Gewinnen der Ethanollösung und Abkühlen der genannten Lösung auf eine Temperatur
von etwa Raumtemperatur, um Lycopinkristalle zu erhalten, und
- Filtrieren der genannten Lösung, um die Lycopinkristalle zu gewinnen.
2. Verfahren nach Anspruch 1, bei dem die Entfernung der Verunreinigungen für 5 bis 40
min durchgeführt wird.
3. Verfahren nach irgendeinem der Ansprüche 1 oder 2, bei dem zur Entfernung der Verunreinigungen
das Verhältnis Ethanol/Produkt etwa 15:1 beträgt.
4. Verfahren nach irgendeinem der Ansprüche 1 bis 3, bei dem das Entfernen der Verunreinigungen
mit zwei Ethanolbehandlungen durchgeführt wird.
5. Verfahren nach irgendeinem der Ansprüche 1 bis 4, bei dem die Extraktion des gereinigten
Produkts innerhalb von 2 bis 10 min mit Ethanol mit einem Alkoholgehalt von 94% durchgeführt
wird.
6. Verfahren nach Anspruch 5, bei dem zwei Extraktionen mit Ethanol durchgeführt werden.
7. Verfahren nach irgendeinem der Ansprüche 1 bis 6, bei dem die Gewinnung der Lycopinkristalle
bei einer Temperatur zwischen 4°C und Raumtemperatur während 2 bis 12 h durchgeführt
wird.
1. Procédé pour l'extraction du lycopène d'un produit choisi dans le groupe consistant
en la tomate, le marc de tomate, le pamplemousse rose, la pastèque, la goyave et la
papaye, ledit procédé comprenant les étapes consistant :
- à éliminer les impuretés et l'eau du produit en soumettant le produit à au moins
un lavage avec de l'éthanol bouillant, ledit éthanol ayant une teneur en eau de 20
à 30 %,
- à extraire le produit purifié en soumettant ledit produit à au moins une extraction
avec de l'éthanol bouillant ayant une teneur en alcool d'au moins 92 %,
- à recueillir la solution éthanolique et refroidir ladite solution à une température
proche de la température ambiante pour obtenir des cristaux de lycopène, et
- à filtrer ladite solution pour recueillir les cristaux de lycopène.
2. Procédé suivant la revendication 1, dans lequel l'élimination des impuretés est effectuée
pendant un temps de 5 à 40 minutes.
3. Procédé suivant l'une quelconque des revendications 1 et 2, dans lequel, pour l'élimination
des impuretés, le rapport éthanol/produit est égal à environ 15:1.
4. Procédé suivant l'une quelconque des revendications 1 à 3, dans lequel l'élimination
des impuretés est effectuée par deux traitements avec de l'éthanol.
5. Procédé suivant l'une quelconque des revendications 1 à 4, dans lequel l'extraction
du produit purifié est effectuée pendant un temps de 2 à 10 minutes avec un éthanol
ayant une teneur en alcool de 94 %.
6. Procédé suivant la revendications 5, dans lequel deux extractions sont effectuées
avec de l'éthanol.
7. Procédé suivant l'une quelconque des revendications 1 à 6, dans lequel les cristaux
de lycopène sont recueillis à une température comprise dans l'intervalle de 4 °C à
la température ambiante pendant un temps de 2 à 12 heures.